EP2658651B1 - Compositions à base de nickel pour la préparation de nickel métallique et de complexes de nickel - Google Patents

Compositions à base de nickel pour la préparation de nickel métallique et de complexes de nickel Download PDF

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EP2658651B1
EP2658651B1 EP10838214.4A EP10838214A EP2658651B1 EP 2658651 B1 EP2658651 B1 EP 2658651B1 EP 10838214 A EP10838214 A EP 10838214A EP 2658651 B1 EP2658651 B1 EP 2658651B1
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nickel
ions
carbonate
ligand
reaction mixture
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EP2658651A1 (fr
EP2658651A4 (fr
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John J. Ostermaier
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Invista Textiles UK Ltd
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Invista Textiles UK Ltd
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    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F9/00—Compounds containing elements of Groups 5 or 15 of the Periodic Table
    • C07F9/02—Phosphorus compounds
    • C07F9/06—Phosphorus compounds without P—C bonds
    • C07F9/08—Esters of oxyacids of phosphorus
    • C07F9/141—Esters of phosphorous acids
    • C07F9/145—Esters of phosphorous acids with hydroxyaryl compounds
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02—Impregnation, coating or precipitation
    • B01J37/03—Precipitation; Co-precipitation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74—Iron group metals
    • B01J23/755—Nickel
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
    • B01J31/18—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms
    • B01J31/1845—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms the ligands containing phosphorus
    • B01J31/185—Phosphites ((RO)3P), their isomeric phosphonates (R(RO)2P=O) and RO-substitution derivatives thereof
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/16—Reducing
    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G53/00—Compounds of nickel
    • C01G53/06—Carbonates
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C253/00—Preparation of carboxylic acid nitriles
    • C07C253/08—Preparation of carboxylic acid nitriles by addition of hydrogen cyanide or salts thereof to unsaturated compounds
    • C07C253/10—Preparation of carboxylic acid nitriles by addition of hydrogen cyanide or salts thereof to unsaturated compounds to compounds containing carbon-to-carbon double bonds
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2231/00—Catalytic reactions performed with catalysts classified in B01J31/00
    • B01J2231/30—Addition reactions at carbon centres, i.e. to either C-C or C-X multiple bonds
    • B01J2231/32—Addition reactions to C=C or C-C triple bonds
    • B01J2231/322—Hydrocyanation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
    • B01J2531/80—Complexes comprising metals of Group VIII as the central metal
    • B01J2531/84—Metals of the iron group
    • B01J2531/847—Nickel

Definitions

  • the invention relates to a method of making a nickel complex with phosphorous-containing ligands. Described are nickel compositions for use in manufacturing nickel metal compositions, and methods of making basic nickel carbonates (BNC) used to produce nickel metal compositions.
  • the nickel metal compositions can be used to produce nickel catalyst complexes with phosphorous-containing ligands.
  • Hydrocyanation catalyst systems particularly pertaining to the hydrocyanation of ethylenically unsaturated compounds, are known in the art.
  • systems useful for the hydrocyanation of 1,3-butadiene (BD) to form pentenenitrile (PN) and in the subsequent hydrocyanation of pentenenitrile to form adiponitrile (ADN) are known in the commercially important nylon synthesis field.
  • hydrocyanation of activated ethylenically unsaturated compounds proceeds without the use of a Lewis acid promoter, while hydrocyanation of unactivated ethylenically unsaturated compounds, such as 1-octene and 3-pentenenitrile (3PN), requires the use of a Lewis acid promoter.
  • conjugated ethylenically unsaturated compounds e.g., BD and styrene
  • strained ethylenically unsaturated compounds e.g., norbornene
  • U.S. Patent No. 3,903,120 describes the preparation of zerovalent nickel complexes of the types Ni(MZ 3 ) 4 and Ni(MZ 3 ) 2 A; wherein M is P, As or Sb; Z is R or OR, wherein R is an alkyl or aryl radical having up to 18 carbon atoms and may be the same or different, and at least one Z is OR; A is a monoolefinic compound having 2 to 20 carbon atoms; the R radicals of a given MZ 3 of Ni(MZ 3 ) 2 A preferably being so chosen that the ligand has a cone angle of at least 130°; are prepared by reacting elemental nickel with the monodentate MZ 3 ligand at a temperature in the range of 0°C-150°C in the presence of a halogen-containing derivative of the monodentate MZ 3 ligand as a catalyst. A more rapid reaction is realized by carrying out the preparation in an organonitrile solvent.
  • U.S. Patent No. 4,416,825 also describes an improved, continuous process for the preparation of hydrocyanation catalysts comprising zerovalent nickel complexes with monodentate organophosphorus compounds (ligands) by controlling the temperature of the reaction relative to the amount of monodentate ligand and conducting the reaction in the presence of a chlorine ion and organic nitrile such as adiponitrile.
  • ligands monodentate organophosphorus compounds
  • European Patent No. 0,985,448 describes the preparation of nickel catalysts with a high nickel loading, a high nickel surface area, good sinter resistance and wide pores. This is achieved by including a structural promoter, such as silica, silica-alumina, alumina, zirconia, titania, magnesia or ceria, in the catalyst during the preparation thereof.
  • a structural promoter such as silica, silica-alumina, alumina, zirconia, titania, magnesia or ceria
  • Ni(COD) 2 nickel bis(1,5-cyclooctadiene)
  • a phosphite ligand there are several processes that can be used to make nickel catalyst complexes with phosphorous-containing ligands.
  • One method is a reaction between nickel bis(1,5-cyclooctadiene) [NI(COD) 2 ] and a phosphite ligand; however, this process is not very economical because of the high costs of Ni(COD) 2 .
  • Another process involves the in situ reduction of anhydrous nickel chloride with zinc dust in the presence of the phosphite ligand. For this reaction to be successful, the nickel metal must react with the phosphorous-containing ligand at a sufficient rate to produce the nickel complex.
  • U.S. Patent No. 6,171,996 describes zero-valent nickel complexes comprising bidentate phosphite ligands prepared or generated according to techniques well known in the art, as described, for example, in U.S. Patent Nos. 3,496,217 ; 3,631,191 ; 3,846,461 ; 3,847,959 and 3,903,120 .
  • divalent nickel compounds may be combined with a reducing agent, to serve as a source of zero-valent nickel in the reaction.
  • Suitable divalent nickel compounds are said to include compounds of the formula NiY 2 where Y is halide, carboxylate, or acetylacetonate.
  • Suitable reducing agents are said to include metal borohydrides, metal aluminum hydrides, metal alkyls, Zn, Fe, Al, Na, or H 2 .
  • bidentate phosphorus-containing ligands In comparison to monodentate phosphorus-containing ligands, bidentate phosphorus-containing ligands generally react more slowly with nickel metals described in the above references.
  • nickel metal is the INCO type 123 nickel metal powder ( Chemical Abstract Service registry number 7440-02-0 ), derived from the decomposition of nickel carbonyl at elevated temperatures.
  • BNC basic nickel carbonate
  • Bidentate ligands may be converted to nickel catalysts that have certain advantages over the nickel catalysts comprising monodentate ligands, especially as olefin hydrocyanation catalysts.
  • the INCO type 123 nickel metal powders have insufficient reactivity with the some of these bidentate ligands. Therefore, a nickel metal powder that is sufficiently reactive with bidentate phosphorous ligands and methods of making the nickel metal powder is desirable.
  • BNC Basic nickel carbonate
  • a basic nickel carbonate which yields a nickel metal that is highly reactive with both monodentate and bidentate phosphorous-containing ligands in forming nickel metal complexes. Also described are methods of making the basic nickel carbonate, since it has also been discovered that precipitation conditions for making the basic nickel carbonate influence the activity of the resulting nickel metal.
  • the resulting nickel metal is useful in forming nickel metal complexes for producing pentenenitriles and dinitriles by hydrocyanation.
  • the present invention provides a method of making a nickel complex with phosphorous containing ligands, comprising: (i) providing a basic nickel carbonate; and (ii) reducing at least a portion of the basic nickel carbonate of step (i) with a reducing agent to form a nickel-containing solid comprising nickel metal; (iii) reacting the nickel-containing solid with a bidentate phosphorous-containing ligand to form the nickel complex; wherein step (i) comprises: (a) contacting a precipitant solution with a nickel solution in a precipitation reactor to form a reaction mixture; (b) precipitating a basic nickel carbonate from said reaction mixture; wherein said nickel solution comprises nickel(II) ions and water and said precipitant solution is selected from the group consisting of: (i) bicarbonate ions and water, (ii) carbonate ions and water, and (iii) mixtures thereof; and further wherein the mole ratio of bicarbonate ions to nickel ions in the reaction mixture is between 0:1 to
  • the precipitant solution is added to the nickel solution, for example, by gradual addition.
  • Monodentate A single phosphorous atom that may bond to a single nickel atom to form the nickel complex.
  • Bidendate Two phosphorous atoms that may bond to a single nickel atom to form the nickel complex.
  • Phosphite An organophosphorous compound comprising a trivalent phosphorous atom bonded to three oxygen atoms.
  • Phosphonite An organophosphorous compound comprising a trivalent phosphorous atom bonded to two oxygen atoms and one carbon atoms.
  • Phosphinite An organophosphorous compound comprising a trivalent phosphorous atom bonded to one oxygen atoms and two carbon atoms.
  • Phosphine An organophosphorous compounding comprising a trivalent phosphorous atom bonded to three carbon atoms.
  • the nickel complexes with phosphorous containing ligands can be made by (i) providing a basic nickel carbonate; and (ii) reducing at least a portion of the basic nickel carbonate of step (i) with a reducing agent to form a nickel-containing solid comprising nickel metal; (iii) reacting the nickel-containing solid with a bidentate phosphorous-containing ligand to form the nickel complex; wherein step (i) comprises: (a) contacting a precipitant solution with a nickel solution in a precipitation reactor to form a reaction mixture; (b) precipitating a basic nickel carbonate from said reaction mixture, wherein said nickel solution comprises nickel(II) ions and water and said precipitant solution is selected from the group consisting of: (i) bicarbonate ions and water, (ii) carbonate ions and water, and (iii) mixtures thereof.
  • the mole ratio of bicarbonate ions to nickel ions in the reaction mixture at the conclusion of said feeding can range from 0:1 to 2:1, including from 0:1 to 1.6:1, from 0:1 to 1.2:1, from 1.0:0 to 1.9:1, from 1.2:1 to 1.9:1, from 0.8:1 to 1.4:1, from 1.0:1 to 1.8:1, from 1.0:1 to 1.6:1, from 1.0:1 to 1.4:1, from 0.8:1 to 1.4:1, and from 0.8:1 to 1.2:1.
  • the mole ratio of carbonate ions to nickel ions in the reaction mixture at the conclusion of said feeding can range from 0:1 to 1.6:1, including from 0:1 to 1.4:1, from 1.0:0 to 1.2:1, from 0.8:1 to 1.4:1, from 1.0:1 to 1.6:1, from 1.0:1 to 1.6:1, from 1.0:1 to 1.4:1, from 0.8:1 to 1.4:1, and from 0.8:1 to 1.2:1.
  • Blends of bicarbonates and carbonates can also be used in the precipitant solution.
  • the molar ratio has a surprising effect on the resulting nickel metal's effectiveness of reacting with the phosphorous ligands.
  • the precipitation reactor may be any suitable containment vessel such as a tank or pipe. Further, the reaction mixture may be agitated prior to and/or during the precipitation of the basic nickel carbonate. For example, agitation may be done by mechanical stirring, pumped circulation loop, flow-through static mixture, or ultrasound.
  • the basic nickel carbonate may be precipitated within a temperature range of from 0oC to 90oC, including from 20oC to 90oC, from 20oC to 70oC, from 20oC to 50oC, from 50oC to 90oC, from 60oC to 80oC, and from 65oC to 75oC. Furthermore, the basic nickel carbonate may be precipitated from the reaction mixture in the presence of added carbon dioxide.
  • the carbon dioxide can be added to the precipitation reactor, added to the nickel solution, added to the precipitant solution, or added to the reaction mixture, and any combination thereof.
  • the precipitant solution may be fed over a period of from 30 minutes to 60 minutes, and can be done in a semi-continuous or continuous manner.
  • the precipitant solution can be added to the nickel solution in the precipitation reactor in a semi-continuous or continuous manner, for example, gradual addition.
  • the reaction mixture may also be digested after contacting the precipitant solution to the nickel solution by heating the reaction mixture from between 50oC and 90oC for a period of from 0.25 hours to 24 hours.
  • Other suitable temperature ranges include from 60oC to 80oC and from 65oC to 75oC.
  • Other suitable time periods can range from 2 hours to 24 hours, including from 4 hours to 20 hours, from 6 hours to 16 hours, and from 8 hours to 12 hours.
  • the disclosed methods for preparing a nickel complex with phosphorous containing ligands can further comprise, after the precipitation step, washing the precipitated basic nickel carbonate with water; and partially drying the precipitated basic nickel carbonate.
  • the precipitated basic nickel carbonate from the reaction mixture is separated from the reaction mixture by filtration or decantation, the resulting precipitated basic nickel carbonate is washed with water by filtration or decantation, and the resulting precipitated basic nickel carbonate is dried by water evaporation between 60oC and 100°C. Drying can be performed under ambient pressure or under vacuum, and in the presence of an inert gas such as nitrogen.
  • the nickel solution comprising nickel(II) ions and water, may be prepared by dissolving a nickel(II) salt in water.
  • the nickel salt can be any salt that is soluble in water, for example NiCl 2 , NiSO 4 , and Ni(NO 3 ) 2 .
  • the precipitant solution, comprising bicarbonate ions may be prepared by dissolving a bicarbonate salt, for example, NaHCO 3 and NH 4 HCO 3 , in water or prepared in-situ by dissolving CO 2 and an alkali metal hydroxide or ammonia in water by known methods.
  • the precipitant solution comprising carbonate ions
  • the anion of the nickel salt and cation of the bicarbonate or carbonate salt may be selected such that a salt produced from the precipitation, comprising both the cation and anion from the reaction mixture (for example NaCl), is soluble in the water of the reaction mixture.
  • a salt produced from the precipitation comprising both the cation and anion from the reaction mixture (for example NaCl)
  • Such a selection provides a method for separating said salt product from the precipitated basic nickel carbonate.
  • a method of making a nickel-containing solid comprising nickel metal comprises: (i) providing the basic nickel carbonates disclosed above; and (ii) reducing at least a portion of the basic nickel carbonate of step (i) with a reducing agent to form a nickel-containing solid, comprising nickel metal, wherein said nickel-containing solid is adapted to effectively react with a bidendate phosphorous containing ligand to form a nickel complex of the phosphorous-containing ligand.
  • the nickel-containing solid is more reactive with phosphorous-containing ligands than nickel-containing solids made by other processes, such as INCO type 123 nickel metal powder, nickel oxide, nickel formate, nickel oxalate, nickel hydroxide, nickel carbonate.
  • the high reactivity is partially due to the BNC processes disclosed above, as well as the reducing process.
  • the reducing agent can be hydrogen, carbon dioxide, carbon monoxide, methane, ammonia, hydrogen sulfide, merely to name a few nonlimiting examples of suitable reducing agents.
  • the amount of bicarbonate or carbonate ions fed relative to the nickel(II) ions charged greatly affects the reactivity of the resulting nickel-containing solid with the phosphorous-containing ligand to make a nickel complex.
  • producers of BNC-type nickel compositions would be led to add excess amounts of the precipitant solution so as to recover as much of the nickel as economically feasible.
  • the use of excess precipitant produces nickel metal of low reactivity for the phosphorous-ligand complex reaction. Highly reactive nickel is produced when reduced levels of precipitant are used, and presumably more of the nickel(II) ions are allowed to remain dissolved in the water of the resulting reaction mixture.
  • the precipitated basic nickel carbonate made using bicarbonate ions filters and washes much faster than the precipitated basic nickel carbonate made using carbonate ions. Also, the filtered precipitated basic nickel carbonate made using bicarbonate ions dries to a soft powder with little shrinkage. For these reasons, producing the nickel-containing solid using bicarbonate ions provides further desirable properties for downstream processing and handling of the dried precipitated basic nickel carbonate.
  • the reduction of the basic nickel carbonate with a reducing agent to form a nickel-containing solid may be performed at a temperature in the range from 150oC to 700oC, including from 300oC to 500oC, and from 350oC to 450oC.
  • the reduction temperature is from 350 oC to 1500oC, including from 350oC to 450oC.
  • the reduction pressure can range from 0.01 atmospheres to 100 atmospheres.
  • Reduction may be carried out for a period of at least about 30 minutes using a stoichiometric excess of a reducing agent, such as hydrogen, even though one mole of hydrogen per mole of nickel composition is the theoretical and stiochiometric amount required for reduction.
  • the reducing period can be between 1 to 2 hours using a 2:1 mole ratio of hydrogen to nickel composition.
  • the nickel containing solids are reacted with a phosphorous-containing ligand to make a nickel complex of the phosphorous-containing ligand.
  • Such complexes are useful as a catalyst precursor for at least one of the following reactions:
  • the phosphorous-containing ligand may be a monodentate phosphite, stagentate phosphonite, monodentate phosphinite, monodentate phosphine, bidentate phosphite, bidentate phosphonite, bidentate phosphinite, or bidentate phosphine, and any combination of these members. Further, the phosphorous-containing ligand may be a monodentate phosphite to form the nickel complex of the monodentate phosphite then the nickel complex of the monodentate phosphite may be combined with a bidentate phosphorous-containing ligand. Likewise, the phosphorous-containing ligand may be a bidentate phosphite further comprising a monodentate phosphite.
  • the bidentate phosphite may be selected from the members of the groups consisting of Formula la, Formula Ib, Formula Ic, or any combination of these members: wherein in Formulae la, Ib, and Ic, R 1 is phenyl, unsubstituted or substituted with one or more C 1 to C 12 alkyl, C 1 to C 12 alkoxy groups, or groups of Formulae A and B, or -(CH 2 ) n OY 2 ; or naphthyl, unsubstituted or substituted with one or more C 1 to C 12 alkyl or C 1 to C 12 alkoxy groups, or groups of Formulae A and B, or -(CH 2 ) n OY 2 ; or 5,6,7,8-tetrahydro-1-naphthyl; wherein in Formulae A and B, Y 1 is independently selected from the group of H, C 1 to C 18 alkyl
  • the bidentate phosphite may be selected from the group consisting of Formula VII and VIII, wherein,
  • the bidentate phosphite may be selected from the group consisting of Formula IX wherein R 17 is isopropyl, R 18 is hydrogen, and R 19 is methyl; and Formula X wherein R 17 is methyl, R 18 is methyl, and R 19 is hydrogen.
  • the reacting of the nickel-containing solid with the monodentate phosphorus-containing ligand may further comprise at least one halogenated catalyst comprising a phosphorus-halide bond selected from the group consisting of PX 3 , R 17 PX 2 , R 18 OPX 2 , [R 19 ][R 21 ]PX, [R 21 ][R 22 O]PX, and [R 23 O][R 24 O]PX; wherein R 17 , R 18 , R 19 , R 20 , R 21 , R 22 , R 23 , and R 24 are independently selected from the group consisting of C 1 to C 18 hydrocarbyl radicals and each X is a halide independently selected from the group consisting of chloride, bromide, and iodide
  • the bidentate phosphorous containing ligands can further comprise at least one Lewis acid promoter.
  • the Lewis acid may be selected from the group consisting of inorganic or organometallic compounds in which the cation is selected from the group including scandium, titanium, vanadium, chromium, manganese, iron, cobalt, copper, zinc, boron, aluminum, yttrium, zirconium, niobium, molybdenum, cadmium, rhenium, lanthanum, europium, ytterbium, tantalum, samarium, and tin.
  • the at least one Lewis acid is selected from the group consisting of zinc chloride, ferrous chloride, or a combination of zinc chloride and ferrous chloride.
  • the reaction between the nickel-containing solid and the phosphorous-containing ligand may further comprise an organonitrile selected from one or more members of the group consisting of 2-pentenenitrile, 3-pentenenitrile, 4-pentenenitrile, 2-methyl-3-butenenitrile, 2-methyl-2-bytenenitrile, adiponitrile, 2-metylglutaronitrile, and ethylsuccinotrile.
  • organonitrile selected from one or more members of the group consisting of 2-pentenenitrile, 3-pentenenitrile, 4-pentenenitrile, 2-methyl-3-butenenitrile, 2-methyl-2-bytenenitrile, adiponitrile, 2-metylglutaronitrile, and ethylsuccinotrile.
  • Nickel complex or nickel complexes from the reaction of monodentate and bidentate ligands with the nickel-containing solids of this invention may be performed as described in U.S. Provisional Application No. 61/287,757 and the following Examples.
  • a 5 wt% solution of a bidentate phosphorus-containing ligand in pentenenitrile solvent further comprising a Lewis acid like ZnCl 2 (0.5 to 2.5 moles Lewis acid per mole bidentate phosphorus-containing ligand) is contacted with the nickel-containing solid of the invention (for example, 4.0 wt% nickel-containing solid).
  • Temperatures between 60°C and 80°C give acceptable reaction rates. Sufficient agitation may be used to suspend the nickel-containing solid in this reaction mixture.
  • ADN adiponitrile
  • BD 1,3-butadiene
  • hrs hours
  • BNC basic nickel carbonate
  • 2M3BN 2-methyl-3-butenenitrile
  • MGN 2-methylglutaronitrile
  • pentenenitrile or pentenenitriles 4PN, 3PN, 2PN, 2M3BN, and 2M2BN isomers unless specifically limited
  • 2PN 2-pentenenitrile including both c2PN and t2PN isomers unless specifically limited
  • 3PN 3-pentenenitrile including both c3PN and t3PN unless specifically limited
  • 4PN 4-pentenenitrile
  • ppm parts per million by weight
  • wt% % by weight.
  • Ligand A may be prepared by any suitable synthetic means known in the art.
  • 3,3'-diisopropyl-5,5',6,6'-tetramethyl-2,2'-biphenol can be prepared by the procedure disclosed in U. S. Published Patent Application No. 2003/0100802 in which 4-methylthymol can undergo oxidative coupling to the substituted biphenol in the presence of a copper chlorohydroxide-TMEDA complex (TMEDA is N,N,N',N'-tetramethylethylenediamine) and air.
  • TEDA is N,N,N',N'-tetramethylethylenediamine
  • the phosphorochloridite of 2,4-xylenol, [(CH 3 ) 2 C 6 H 3 O] 2 PCl can be prepared, for example, by the procedure disclosed in U.S. Published Patent Application No. 2004/0106815 .
  • anhydrous triethylamine and 2,4-xylenol can be added separately and concurrently in a controlled manner to PCl 3 dissolved in an appropriate solvent under temperature-controlled conditions.
  • the reaction of this phosphorochloridite with the 3,3'-diisopropyl-5,5',6,6'-tetramethyl-2,2'-biphenol to form the desired Ligand A can be performed, for example, according to the method disclosed in U.S.
  • Patent No. 6,069,267 The phosphorochloridite can be reacted with 3,3'-diisopropyl-5,5',6,6'-tetramethyl-2,2'-biphenol in the presence of an organic base to form Ligand A, which can be isolated according to techniques well known in the art, for example as also described in U.S. Patent No. 6,069,267 .
  • Ligand A is an example of a compound of Formula I and the Ligand A solutions in 3PN solvent below do not contain any halogenated catalysts of U.S. Patent No. 3,903,120 .
  • Example 16 uses a mixture of different monodentate phosphites, Ligand B, that is derived from the reaction of a m-cresol/p-cresol/phenol mixture with PCl 3 .
  • a 1 molar NiCl 2 solution (250 mL, 0.25 mole NiCl 2 ) in water is charged to a 1 liter beaker then this solution is magnetically stirred with heating to 70°C. While maintaining this temperature, a precipitant solution comprising bicarbonate ions (25.2 gm of NaHCO 3 dissolved in 400 mL water, 0.30 mole NaHCO 3 ) is fed continuously into the beaker at a rate of 10 mL/min as the reaction mixture is sparged with added CO 2 gas at a rate of 100 mL/min. At the conclusion of the precipitant solution addition, the total moles of bicarbonate ions fed per mole of nickel ions charged is 1.2:1.
  • This addition causes a solid product, a BNC composition comprising nickel, to precipitate from the reaction mixture.
  • a solid product a BNC composition comprising nickel
  • the flow of carbon dioxide gas to the reaction mixture is then terminated and the resulting reaction mixture slurry is then allowed to digest for 2 hours at 70°C.
  • this slurry is then filtered using a sintered glass filter, and the solid filter cake is displacement washed with 200 mL water.
  • the solid filter cake is then dried in a vacuum oven at 80°C overnight while sweeping nitrogen through the vacuum oven.
  • reaction tube Fifteen grams of the dried solid filter cake is then placed inside a reaction tube that can be heated within an electrical furnace located in a lab fume hood. Hydrogen gas flow to the reaction tube is then set at 0.2 liters/minute (about one atmosphere) with any hydrogen off gas from the reaction tube flowing through a bubbler. The temperature of the tube furnace is then increased at a rate of 10°C/minute to a final temperature of 400°C, and then held for one hour at 400°C, after which the reaction tube is allowed to cool under hydrogen flow. After the reaction tube temperature falls below 50°C the flow to the reaction tube is switched to nitrogen gas to purge the hydrogen from the reaction tube.
  • Valves on the reaction tube were then closed to prevent exposure of the resulting nickel-containing solid, comprising nickel metal, to air, and the entire reaction tube is transferred to a nitrogen-filled dry lab and the nickel-containing solid emptied into a bottle.
  • This nickel-containing solid contains nickel metal as it is attracted to magnets. Exposing these nickel-containing solids to air can reduce rates for the following reaction and/or cause the nickel-containing solids to burn in air to form nickel oxide.
  • Nickel complexes are also prepared in this nitrogen-filled dry lab by placing 3.2 gm of this nickel-containing solid, 80 gm of a 5 wt% Ligand A solution in 3PN, and 0.50 gm of anhydrous ZnCl 2 , into a bottle reactor that contained a magnetic stir bar. The nickel-containing solid is not soluble in this reaction mixture. With magnetic stirring, the reaction mixture is then heated rapidly to 80°C, and a filtered sample is withdrawn from this reaction mixture after 30 minutes and is found to contain 1460 ppm nickel, according to a UV-visible or LC analysis, as nickel complexes of Ligand A dissolved in the 3PN.
  • a calibrated absorption method that detects the soluble divalent nickel complex (Ligand A)Ni( ⁇ 3 -C 4 H 7 )C ⁇ N-ZnCl 2 by the amount of absorption at a wavelength of 380 nanometers is used.
  • This absorption method is calibrated against a LC analysis for total soluble nickel.
  • Example 1 The general procedure of Example 1 is repeated in Examples 2 to 5, except that the total moles of bicarbonate ions fed per mole of nickel ions charged is varied from 1.6:1 to 2.0:1 by adjusting the amount of NaHCO 3 dissolved in the 400 mL water to prepare the precipitant solution.
  • Results from the reaction of the resulting nickel-containing solids with the Ligand A solution and ZnCl 2 are provided in Table 1.
  • Table 1 Effect of the First Molar Ratio, Moles Bicarbonate Ions Fed/Mole Nickel Ions Charged, on the Reaction of the Resulting Nickel-Containing Solid with Ligand A and ZnCl 2 to Produce Nickel Complexes of Ligand A.
  • Precipitant Solution Example gm NaHCO3 mole NaHCO3 Moles HCO3 Ions Fed/Mole Ni Ions Charged ppm Ni* 1 25.2 0.30 1.2 1460 2 33.6 0.40 1.6 1390 3 37.8 0.45 1.8 1060 4 39.3 0.47 1.9 823 5 42.0 0.50 2.0 92 *As nickel complexes of Ligand A dissolved in the 3PN.
  • Examples 1 through 5 illustrate that as the amount of bicarbonate ions fed is increased relative to the nickel ions charged, there is a decline in the reactivity of the resulting nickel-containing solid with a phosphorus-containing ligand to form soluble nickel complexes. That is, greater amounts of nickel complexes are formed when this first molar ratio, moles bicarbonate ions fed/mole nickel ions charged, is between 0.0:1 and 2.0:1.
  • Example 2 is repeated except in the absence of sparging CO 2 gas through the reaction mixture during the feeding of the sodium bicarbonate solution to the 1liter beaker comprising the nickel ions.
  • Table 2 greater amounts of nickel complexes are formed from the reaction of the resulting nickel-containing solid with the Ligand A solution and ZnCl 2 when the solid product precipitates in the presence of added CO 2 gas.
  • Table 2 Effect of the Presence of Added CO 2 Gas During the Precipitation of the Solid Product on the Reaction of the Resulting Nickel-Containing Solid with Ligand A and ZnCl 2 to Produce Nickel Complexes of Ligand A.
  • Precipitant Solution Example gm NaHCO3 mole NaHCO3 Moles HCO3 Ions Fed/Mole Ni Ions Charged ppm Ni* 2 33.6 0.40 1.6 1390 6 33.6 0.40 1.6 965 *As nickel complexes of Ligand A dissolved in the 3PN.
  • Example 2 is repeated except that temperatures of the heated NiCl 2 solution, reaction mixture during continuous feeding of the precipitant solution to the 1 liter beaker, and digestion period are 50°C for Example 7 and 90°C for Example 8.
  • Example 2 see Table 3
  • greater amounts of nickel complexes are formed from the reaction of the resulting nickel-containing solid with the Ligand A solution and ZnCl 2 when the solid product precipitates at 70°C rather than 50°C or 90°C.
  • Table 3 Effect of Precipitation Temperature on the Reaction of the Resulting Nickel-Containing Solid with Ligand A and ZnCl 2 to Produce Nickel Complexes of Ligand A.
  • Example Heated NiCl 2 Solution Reaction Mixture Digestion Period ppm Ni* 2 70°C 70°C 70°C 1390 7 50°C 50°C 50°C 845 8 90°C 96°C 90°C 850 *As nickel complexes of Ligand A dissolved in the 3PN according to an analysis.
  • Example 2 is repeated except substituting NiSO 4 for NiCl 2 . That is, continuously feeding the precipitant solution of Example 2 to a 1molar NiSO 4 solution (250 mL, 0.25 mole NiSO 4 ) in water at 70°C. Similar to solid product precipitated from NiCl 2 , equivalent amounts of nickel complexes are formed (1465 ppm nickel) after 30 minutes from the reaction of the resulting nickel-containing solid with the Ligand A solution and ZnCl 2 when the solid product precipitates from the NiSO 4 solution.
  • NiSO 4 for NiCl 2 . That is, continuously feeding the precipitant solution of Example 2 to a 1molar NiSO 4 solution (250 mL, 0.25 mole NiSO 4 ) in water at 70°C. Similar to solid product precipitated from NiCl 2 , equivalent amounts of nickel complexes are formed (1465 ppm nickel) after 30 minutes from the reaction of the resulting nickel-containing solid with the Ligand A solution and ZnCl 2 when the solid product precipitates from the NiSO 4 solution
  • a 1 molar NiSO 4 solution (250 mL, 0.25 mole NiSO 4 ) in water is charged to a 1 liter beaker then this solution is magnetically stirred with heating to 70°C. While maintaining this temperature, a precipitant solution comprising carbonate ions (21.2 gm of Na 2 CO 3 dissolved in 400 mL water, 0.20 mole Na 2 CO 3 ) is fed continuously into the beaker at a rate of 10 mL/min but no CO 2 gas is sparged into the reaction mixture. At the conclusion of the precipitant solution addition, the total moles of carbonate ions fed per mole of nickel ions charged is 0.8. This addition also causes a solid product to precipitate from the reaction mixture.
  • the resulting reaction mixture slurry is then allowed to digest for 2 hours at 70°C. At the conclusion of this digestion period, this slurry is then filtered using a sintered glass filter, and the solid filter cake is displacement washed with 200 mL water. The solid filter cake is then dried in a vacuum oven at 80°C while sweeping nitrogen through the vacuum oven overnight.
  • Example 1 Fifteen grams of the dried solid filter cake is reduced with hydrogen flow at elevated temperatures as described in Example 1. Nickel complexes are also prepared as described in Example 1. A filtered sample is withdrawn from the reaction mixture in the bottle reactor after 30 minutes and is found to contain 1420 ppm nickel, according to a UV-Visible or LC analysis, as nickel complexes of Ligand A dissolved in the 3PN.
  • Example 10 The general procedure of Example 10 is repeated in Examples 11 to 13. The difference being that the total moles of carbonate ions fed per mole of nickel ions charged is varied from 1.0:1 to 1.6:1 by adjusting the amount of Na 2 CO 3 dissolved in the 400 mL water to prepare the precipitant solution. Results from the reaction of the resulting nickel-containing solids with the Ligand A solution and ZnCl 2 are provided in Table 4. Table 4. Effect of the Second Molar Ratio, Moles Carbonate Ions Fed/Mole Nickel Ions Charged, on the Reaction of the Resulting Nickel-Containing Solid with Ligand A and ZnCl 2 to Produce Nickel Complexes of Ligand A.
  • Precipitant Solution Example gm Na2CO3 mole Na2CO3 Moles CO3 Ions Fed/Mole Ni Ions Charged ppm Ni* 10 21.2 0.20 0.8 1420 11 26.5 0.25 1.0 1340 12 31.8 0.30 1.2 1065 13 42.0 0.40 1.6 0 *As nickel complexes of Ligand A dissolved in the 3PN.
  • Examples 10 through 13 illustrate that the reactivity of the resulting nickel-containing solid with a phosphorus-containing ligand to form soluble nickel complexes can decline as the amount of carbonate ions fed is increased relative to the nickel ions charged. That is, greater amounts of nickel complexes are formed when this second molar ratio, moles carbonate ions fed/mole nickel ions charged, is between 0.0 and 1.6.
  • Example 5 is repeated except that the order of addition is reversed for the solid precipitation reaction in the 1 liter beaker. That is, the 1 molar NiCl 2 solution is added to the precipitant solution to precipitate a solid product. After digestion, filtration, displacement washing, drying, reducing with hydrogen gas in the reactor tube at 400°C, followed by reacting the resulting nickel-containing solid with the Ligand A solution in 3PN and ZnCl 2 , the filtered sample withdrawn from the reaction mixture is found to contain 0 ppm nickel as nickel complexes of Ligand A dissolved in the 3PN.
  • the weight of the dried solid filter cake is also a function of the total moles of bicarbonate (Examples 1 to 9, Table 5) or carbonate ions (Examples 10 to 13, Table 6) fed per mole of nickel ions charged. Table 5. Effect of the First Molar Ratio, Moles Bicarbonate Ions Fed/Mole Nickel Ions Charged, on the Weight of the Dried Solid Filter Cake and Reaction of the Resulting Nickel-Containing Solid with Ligand A and ZnCl 2 to Produce Nickel Complexes of Ligand A.
  • Example 1 2 6 7 8 9 3 4 5 14 Precipiating Temperature 70°C 70°C 70°C 50°C 90°C 70°C 70°C 70°C 70°C 70°C Moles HCO3 Ions Fed/Mole Ni Ions Charged 1.2 1.6 1.6 1.6 1.6 1.6 1.8 1.9 2.0 2.0 gm Dried Solid Filter Cake 16.2 21.70 22.1 22.3 15.9 23.5 24.2 26.8 27.6 26.2 ppm Ni* 1460 1390 965 845 850 1465 1060 823 92 0 Table 6.
  • nickel-containing solids of Examples 1 to 13 are reacted with the monodentate phosphite Ligand B in 3PN solvent to form nickel complexes, comprising zero-valent nickel and Ligand B, in the absence of a Lewis acid such as ZnCl 2 .
  • ZnCl 2 is at least partially separated from the nickel complex of Examples 1 to 12 then the nickel complex of Ligand A contacts BD and HC ⁇ N in a reaction zone.
  • a catalyst forms to produce 3PN, 2M3BN, or a combination thereof.
  • the same nickel complexes also react with 2M3BN to produce 3PN.
  • Nickel complexes of Ligand B of Example 16 contact HC ⁇ N and BD in a reaction zone.
  • a catalyst forms to produce 3PN, 2M3BN, or a combination thereof.
  • the same nickel complexes also react with 2M3BN to produce 3PN.
  • the soluble nickel complexes of Ligand A from bottle reactors of Examples 1 to 12 contact HC ⁇ N and 3PN in a reaction zone.
  • a catalyst forms converting greater than 90% of the 3PN to dinitriles comprising ADN, MGN, and ESN, with an ADN distribution of 95-96%.
  • the ADN distribution equals 100% * wt% ADN / (wt% ADN + wt% MGN + wt% ESN), as determined by gas chromatography (GC).
  • the soluble nickel complexes of Ligand A from bottle reactors of Examples 1 to 12 contact HC ⁇ N and 2PN in a reaction zone.
  • a catalyst forms converting a portion of the 2PN to 3PN, 4PN, and ADN.
  • a Lewis acid promoter like ZnCl 2 , triphenylboron, or compounds of the chemical formula [Ni(C 4 H 7 C ⁇ N) 6 ][(C 6 H 5 ) 3 BC ⁇ NB(C 6 H 5 ) 3 ] 2 as disclosed in U.S. Patent No. 4,749,801
  • the nickel complexes of Example 16 contact HC ⁇ N and 3PN in a reaction zone.
  • a catalyst forms converting 3PN to dinitriles comprising ADN, MGN, and ESN, wherein ADN is the major dinitrile product.

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Claims (16)

  1. Procédé de fabrication d'un complexe de nickel avec des ligands contenant du phosphore, comprenant
    (i) la fourniture d'un carbonate de nickel basique ; et
    (ii) la réduction d'au moins une partie du carbonate de nickel basique de l'étape (i) avec un agent réducteur pour former un solide contenant du nickel comprenant du nickel métallique ;
    (iii) la réaction du solide contenant du nickel avec un ligand bidenté contenant du phosphore pour former le complexe de nickel ;
    dans lequel l'étape (i) comprend :
    (a). la mise en contact d'une solution de précipitant avec une solution de nickel dans un réacteur de précipitation pour former un mélange de réaction ;
    (b). la précipitation d'un carbonate de nickel basique à partir dudit mélange de réaction ;
    dans lequel ladite solution de nickel comprend des ions nickel(II) et de l'eau et ladite solution de précipitation est choisie dans le groupe comprenant : (i) des ions bicarbonate et de l'eau, (ii) des ions carbonate et de l'eau et (iii) leurs mélanges ; et en outre dans lequel le rapport molaire des ions bicarbonate aux ions nickel dans le mélange de réaction est compris entre 0:1 et 2:1 et ledit rapport molaire des ions carbonate aux ions nickel dans le mélange de réaction est compris entre 0:1 et 1,6:1.
  2. Procédé selon la revendication 1, dans lequel la mise en contact (a) comprend l'ajout de la solution de précipitation à la solution de nickel.
  3. Procédé selon la revendication 1 ou 2, dans lequel lesdits ions nickel(II) sont choisis dans le groupe constitué de NiCl2, NiSO4 et Ni(NO3)2.
  4. Procédé selon la revendication 2 ou 3, dans lequel lesdits ions nickel(II) sont NiCl2.
  5. Procédé selon la revendication 1 ou 2, dans lequel lesdits ions bicarbonate sont choisis dans le groupe constitué de : NaHCO3 et NH4HCO3.
  6. Procédé selon la revendication 1 ou 2, dans lequel lesdits ions carbonate comprennent Na2CO3.
  7. Procédé selon la revendication 1 ou 2, comprenant en outre la mise en contact dudit mélange de réaction avec du dioxyde de carbone.
  8. Procédé selon la revendication 7, dans lequel ladite mise en contact est effectuée en précipitant ledit carbonate de nickel basique.
  9. Procédé selon l'une des revendications 1 à 8, comprenant en outre la digestion du mélange de réaction avant la précipitation dudit carbonate de nickel basique.
  10. Procédé selon la revendication 9, dans lequel ladite digestion est effectuée à une température de 50 °C à 90 °C et une durée de 0,25 heure à 24 heures.
  11. Procédé selon l'une des revendications 1 à 8, dans lequel ladite précipitation dudit carbonate de nickel basique est effectuée à une température de 0 °C à 90 °C.
  12. Procédé selon la revendication 11, dans lequel ladite température est comprise entre 50 °C et 90 °C.
  13. Procédé selon la revendication 12, dans lequel ladite température est comprise entre 65 °C et 75 °C.
  14. Procédé selon l'une des revendications 1 à 8, dans lequel ledit rapport molaire des ions bicarbonate aux ions nickel peut être choisi dans le groupe constitué de : de 0:1 à 1,6:1, de 0:1 à 1,2:1, de 1,0:1 à 1,9:1, de 0,8:1 à 1,4:1, de 1,0:1 à 1,8:1, de 1,0:1 à 1,6:1, de 1,0:1 à 1,4:1, de 0,8:1 à 1,4:1, et de 0,8:1 à 1,2:1.
  15. Procédé selon l'une des revendications 1 à 8, dans lequel ledit rapport molaire des ions carbonate aux ions nickel peut être choisi dans le groupe constitué de : de 0:1 à 1,4:1, de 1,0:0 à 1,2:1, de 0,8:1 à 1,4:1, de 1,0:1 à 1,6:1, de 1,0:1 à 1,6:1, de 1,0:1 à 1,4:1, de 0,8:1 à 1,4:1, et de 0,8:1 à 1.2:1.
  16. Procédé selon l'une des revendications 1 à 8, comprenant en outre (c) le lavage dudit carbonate de nickel basique précipité avec de l'eau ; et (d) le séchage partiel du carbonate de nickel basique précipité.
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EP2512673B1 (fr) 2016-09-28
EP2658651A1 (fr) 2013-11-06
US20110311428A1 (en) 2011-12-22
EP2512673A4 (fr) 2013-11-20
JP2013514258A (ja) 2013-04-25
DK2658651T3 (en) 2019-01-14
CN102655936A (zh) 2012-09-05
US8815186B2 (en) 2014-08-26
US20110196168A1 (en) 2011-08-11
CN102655936B (zh) 2014-11-05
EP2658651A4 (fr) 2015-11-11
KR20120104252A (ko) 2012-09-20
US9371343B2 (en) 2016-06-21
WO2011075494A1 (fr) 2011-06-23
EP2512673A1 (fr) 2012-10-24
WO2011075496A1 (fr) 2011-06-23

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